US2019352247A1PendingUtilityA1
Two-Phase Reactions in Microdroplets
Assignee: UNIV LELAND STANFORD JUNIORPriority: Feb 10, 2017Filed: Feb 8, 2018Published: Nov 21, 2019
Est. expiryFeb 10, 2037(~10.5 yrs left)· nominal 20-yr term from priority
B05B 7/0846B01J 10/00B01J 14/00C07C 51/255B01J 2204/002B05B 7/0853B01J 4/002B01F 5/0256B01F 3/04049B01F 3/0803B01F 2215/0036B01F 3/0865B01F 23/451B01F 23/405B01F 2101/2204B01J 19/26B01F 23/2132B01F 25/23
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Claims
Abstract
Improved two phase chemical reactions (liquid-liquid or liquid-gas) are provided by forming microdroplets of either or both liquid reagents and configuring the reaction as a collision between the microdroplet reagent and the other reagent. We have found that this approach can provide high reaction yields in short times (<1 s) without the use of a phase transfer catalyst.
Claims
exact text as granted — not AI-modified1 . A method for performing a chemical reaction, the method comprising:
selecting a first liquid reagent; selecting a second liquid reagent, wherein the first liquid reagent and the second liquid reagent are immiscible with respect to each other; nebulizing the first liquid reagent in a first shearing gas flow to provide first microdroplets of the first reagent; configuring the second liquid reagent as second microdroplets of the second reagent in a second shearing gas flow, or as a thin film of the second reagent; directing the first microdroplets at the second reagent to provide a chemical reaction between the first and second liquid reagents by colliding the first microdroplets with the second reagent.
2 . The method of claim 1 , wherein the first microdroplets have a diameter from 0.1 micron to 100 microns.
3 . The method of claim 1 , wherein the second microdroplets have a diameter from 0.1 micron to 100 microns or the thin film of the second reagent has a thickness of 100 microns or less.
4 . The method of claim 1 , wherein the chemical reaction is selected from the group consisting of: C-, N-, O- and S-alkylation; etherification; esterification; transesterification; condensation; carbene reaction; nucleophilic displacement epoxidation; oxidation; and polymerization.
5 . The method of claim 1 , wherein a reaction time of the chemical reaction is 1 second or less.
6 . A method for performing a chemical reaction, the method comprising:
selecting a liquid reagent; selecting a gaseous reagent; nebulizing the liquid reagent in a first shearing gas flow to provide microdroplets of the liquid reagent; directing the microdroplets at the gaseous reagent to provide a chemical reaction between the liquid reagent and the gaseous reagent by colliding the first microdroplets with the gaseous reagent.
7 . The method of claim 6 , wherein the first shearing gas flow is a shearing gas flow of the gaseous reagent.
8 . The method of claim 6 , wherein the gaseous reagent is provided at least in part in a second gas flow distinct from the first shearing gas flow, and wherein the first shearing gas flow and the second gas flow are directed at each other.
9 . The method of claim 8 , wherein the first shearing gas flow is a shearing gas flow of the gaseous reagent.
10 . The method of claim 6 , wherein the microdroplets have a diameter from 0.1 micron to 100 microns.
11 . The method of claim 6 , wherein the chemical reaction is selected from the group consisting of: C-, N-, O- and S-alkylation; etherification; esterification; transesterification; condensation; carbene reaction; nucleophilic displacement epoxidation; oxidation; and polymerization.
12 . The method of claim 6 , wherein a reaction time of the chemical reaction is 1 second or less.Join the waitlist — get patent alerts
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